- InChI
- InChI=1S/C6H4Cl2/c7-5-2-1-3-6(8)4-5/h1-4H
- InChI Key
- ZPQOPVIELGIULI-UHFFFAOYSA-N
- Formula
- C6H4Cl2
- SMILES
- Clc1cccc(Cl)c1
- Molecular Weight1
- 147.00
- CAS
- 541-73-1
- Other Names
-
- 1,3-DICHLOROBENZENE
- Benzene, m-dichloro-
- Metadichlorobenzene
- Rcra waste number U071
- m-Dichlorobenzene
- m-Dichlorobenzol
- m-Phenylene dichloride
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°(+) ion : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
- ΔfH(+) ion,0K : Enthalpy of formation of positive ion at 0K (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-2960.30; -2952.00] | kJ/mol |
|
| ΔcH°liquid | -2960.30 | kJ/mol | NIST |
| ΔcH°liquid | -2955.76 ± 0.96 | kJ/mol | NIST |
| ΔcH°liquid | -2952.00 ± 8.00 | kJ/mol | NIST |
| ΔfG° | 78.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 28.10 | kJ/mol | NIST |
| ΔfH°liquid | -20.50 ± 0.96 | kJ/mol | NIST |
| ΔfH°(+) ion | 903.30 | kJ/mol | NIST |
| ΔfH(+) ion,0K | 915.90 | kJ/mol | NIST |
| ΔfusH° | 13.34 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [47.00; 53.90] | kJ/mol |
|
| ΔvapH° | 53.90 | kJ/mol | NIST |
| ΔvapH° | 47.00 | kJ/mol | NIST |
| IE | [9.10; 9.28] | eV |
|
| IE | 9.10 ± 0.02 | eV | NIST |
| IE | 9.10 ± 0.02 | eV | NIST |
| IE | 9.14 ± 0.03 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.12 ± 0.02 | eV | NIST |
| IE | 9.11 ± 0.01 | eV | NIST |
| IE | 9.12 ± 0.01 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.15 | eV | NIST |
| log10WS | [-3.05; -3.04] |
|
|
| log10WS | -3.05 | Aq. Sol... | |
| log10WS | -3.04 | Estimat... | |
| logPoct/wat | 2.993 | Crippen Calculated Property | |
| McVol | 96.120 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4151.61 | kPa | Joback Calculated Property |
| Inp | [160.40; 1058.00] |
|
|
| Inp | 1017.40 | NIST | |
| Inp | 1020.06 | NIST | |
| Inp | 1027.05 | NIST | |
| Inp | 1027.35 | NIST | |
| Inp | 1013.80 | NIST | |
| Inp | 1022.50 | NIST | |
| Inp | 1022.50 | NIST | |
| Inp | 1036.20 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1024.65 | NIST | |
| Inp | 1004.07 | NIST | |
| Inp | 1013.30 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1014.97 | NIST | |
| Inp | 1015.34 | NIST | |
| Inp | 1017.77 | NIST | |
| Inp | 1018.92 | NIST | |
| Inp | 975.40 | NIST | |
| Inp | 1020.90 | NIST | |
| Inp | 986.21 | NIST | |
| Inp | 985.10 | NIST | |
| Inp | 1002.37 | NIST | |
| Inp | 997.98 | NIST | |
| Inp | 999.87 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | Outlier 162.00 | NIST | |
| Inp | Outlier 160.40 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1017.40 | NIST | |
| Inp | 1022.50 | NIST | |
| Inp | 1004.07 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | Outlier 162.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 975.40 | NIST | |
| Inp | 997.98 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1021.00 | NIST | |
| I | [1409.00; 1477.00] |
|
|
| I | 1455.40 | NIST | |
| I | 1474.10 | NIST | |
| I | 1415.00 | NIST | |
| I | 1415.00 | NIST | |
| I | 1434.00 | NIST | |
| I | 1409.00 | NIST | |
| I | 1414.00 | NIST | |
| I | 1445.33 | NIST | |
| I | 1438.32 | NIST | |
| I | 1417.70 | NIST | |
| I | 1446.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1418.00 | NIST | |
| I | 1409.00 | NIST | |
| I | 1455.40 | NIST | |
| I | 1445.33 | NIST | |
| I | 1453.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1418.00 | NIST | |
| Tboil | [446.15; 446.20] | K |
|
| Tboil | 446.15 | K | KDB |
| Tboil | 446.15 | K | Excess ... |
| Tboil | 446.20 | K | NIST |
| Tboil | 446.15 ± 0.07 | K | NIST |
| Tc | 674.86 | K | Joback Calculated Property |
| Tfus | [246.90; 249.00] | K |
|
| Tfus | 248.39 | K | KDB |
| Tfus | 248.25 | K | Aq. Sol... |
| Tfus | 248.39 ± 0.05 | K | NIST |
| Tfus | 249.00 ± 2.00 | K | NIST |
| Tfus | Outlier 246.90 ± 0.20 | K | NIST |
| Tfus | 248.75 ± 0.50 | K | NIST |
| Vc | 0.361 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.05; 190.77] | J/mol×K | [443.20; 674.86] |
|
| Cp,gas | 149.05 | J/mol×K | 443.20 | Joback Calculated Property |
| Cp,gas | 157.36 | J/mol×K | 481.81 | Joback Calculated Property |
| Cp,gas | 165.09 | J/mol×K | 520.42 | Joback Calculated Property |
| Cp,gas | 172.26 | J/mol×K | 559.03 | Joback Calculated Property |
| Cp,gas | 178.92 | J/mol×K | 597.64 | Joback Calculated Property |
| Cp,gas | 185.08 | J/mol×K | 636.25 | Joback Calculated Property |
| Cp,gas | 190.77 | J/mol×K | 674.86 | Joback Calculated Property |
| Cp,liquid | [167.15; 183.20] | J/mol×K | [283.15; 353.15] |
|
| Cp,liquid | 167.15 | J/mol×K | 283.15 | Heat Ca... |
| Cp,liquid | 167.54 | J/mol×K | 285.15 | Heat Ca... |
| Cp,liquid | 167.93 | J/mol×K | 287.15 | Heat Ca... |
| Cp,liquid | 168.32 | J/mol×K | 289.15 | Heat Ca... |
| Cp,liquid | 168.72 | J/mol×K | 291.15 | Heat Ca... |
| Cp,liquid | 169.13 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 169.55 | J/mol×K | 295.15 | Heat Ca... |
| Cp,liquid | 169.97 | J/mol×K | 297.15 | Heat Ca... |
| Cp,liquid | 170.90 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 170.39 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 170.82 | J/mol×K | 301.15 | Heat Ca... |
| Cp,liquid | 171.25 | J/mol×K | 303.15 | Heat Ca... |
| Cp,liquid | 171.69 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 172.14 | J/mol×K | 307.15 | Heat Ca... |
| Cp,liquid | 172.58 | J/mol×K | 309.15 | Heat Ca... |
| Cp,liquid | 173.04 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 173.49 | J/mol×K | 313.15 | Heat Ca... |
| Cp,liquid | 173.95 | J/mol×K | 315.15 | Heat Ca... |
| Cp,liquid | 174.41 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 174.88 | J/mol×K | 319.15 | Heat Ca... |
| Cp,liquid | 175.35 | J/mol×K | 321.15 | Heat Ca... |
| Cp,liquid | 175.83 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 176.30 | J/mol×K | 325.15 | Heat Ca... |
| Cp,liquid | 176.78 | J/mol×K | 327.15 | Heat Ca... |
| Cp,liquid | 177.26 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 177.75 | J/mol×K | 331.15 | Heat Ca... |
| Cp,liquid | 178.24 | J/mol×K | 333.15 | Heat Ca... |
| Cp,liquid | 178.73 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 179.22 | J/mol×K | 337.15 | Heat Ca... |
| Cp,liquid | 179.71 | J/mol×K | 339.15 | Heat Ca... |
| Cp,liquid | 180.20 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 180.70 | J/mol×K | 343.15 | Heat Ca... |
| Cp,liquid | 181.20 | J/mol×K | 345.15 | Heat Ca... |
| Cp,liquid | 181.70 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 182.20 | J/mol×K | 349.15 | Heat Ca... |
| Cp,liquid | 182.70 | J/mol×K | 351.15 | Heat Ca... |
| Cp,liquid | 183.20 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0002989; 0.0021588] | Pa×s | [256.16; 443.20] |
|
| η | 0.0021588 | Pa×s | 256.16 | Joback Calculated Property |
| η | 0.0012985 | Pa×s | 287.33 | Joback Calculated Property |
| η | 0.0008628 | Pa×s | 318.51 | Joback Calculated Property |
| η | 0.0006166 | Pa×s | 349.68 | Joback Calculated Property |
| η | 0.0004656 | Pa×s | 380.85 | Joback Calculated Property |
| η | 0.0003668 | Pa×s | 412.03 | Joback Calculated Property |
| η | 0.0002989 | Pa×s | 443.20 | Joback Calculated Property |
| ΔfusH | [12.59; 12.64] | kJ/mol | [248.30; 248.75] |
|
| ΔfusH | 12.60 | kJ/mol | 248.30 | NIST |
| ΔfusH | 12.64 | kJ/mol | 248.40 | NIST |
| ΔfusH | 12.64 | kJ/mol | 248.40 | NIST |
| ΔfusH | 12.59 | kJ/mol | 248.75 | NIST |
| ΔvapH | [44.10; 50.40] | kJ/mol | [248.00; 430.50] |
|
| ΔvapH | 50.40 | kJ/mol | 248.00 | NIST |
| ΔvapH | 50.00 | kJ/mol | 262.00 | NIST |
| ΔvapH | 44.10 | kJ/mol | 402.50 | NIST |
| ΔvapH | 44.70 | kJ/mol | 430.50 | NIST |
| n0 | [1.53800; 1.54400] | [298.15; 308.15] |
|
|
| n0 | 1.54400 | 298.15 | Densiti... | |
| n0 | 1.54320 | 298.15 | Liquid-... | |
| n0 | 1.54100 | 303.15 | Densiti... | |
| n0 | 1.53800 | 308.15 | Densiti... | |
| ρl | [1277.16; 1282.87] | kg/m3 | [298.15; 303.15] |
|
| ρl | 1282.87 | kg/m3 | 298.15 | Experim... |
| ρl | 1277.16 | kg/m3 | 303.15 | Effect ... |
| ΔfusS | 50.60 | J/mol×K | 248.75 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.00 | 303.15 | 0.0010 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [324.41; 476.30] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45419e+01 | |||
| Coefficient B | -3.97801e+03 | |||
| Coefficient C | -4.53350e+01 | |||
| Temperature range, min. | 324.41 | |||
| Temperature range, max. | 476.30 | |||
| Pvap | 1.33 | kPa | 324.41 | Calculated Property |
| Pvap | 3.01 | kPa | 341.29 | Calculated Property |
| Pvap | 6.21 | kPa | 358.16 | Calculated Property |
| Pvap | 11.90 | kPa | 375.04 | Calculated Property |
| Pvap | 21.41 | kPa | 391.92 | Calculated Property |
| Pvap | 36.49 | kPa | 408.79 | Calculated Property |
| Pvap | 59.30 | kPa | 425.67 | Calculated Property |
| Pvap | 92.49 | kPa | 442.55 | Calculated Property |
| Pvap | 139.10 | kPa | 459.42 | Calculated Property |
| Pvap | 202.64 | kPa | 476.30 | Calculated Property |
| Pvap | [6.34e-03; 4015.15] | kPa | [248.39; 683.95] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.72737e+01 | |||
| Coefficient B | -7.22933e+03 | |||
| Coefficient C | -6.05176e+00 | |||
| Coefficient D | 2.34995e-06 | |||
| Temperature range, min. | 248.39 | |||
| Temperature range, max. | 683.95 | |||
| Pvap | 6.34e-03 | kPa | 248.39 | Calculated Property |
| Pvap | 0.26 | kPa | 296.79 | Calculated Property |
| Pvap | 3.47 | kPa | 345.18 | Calculated Property |
| Pvap | 22.39 | kPa | 393.58 | Calculated Property |
| Pvap | 91.20 | kPa | 441.97 | Calculated Property |
| Pvap | 271.65 | kPa | 490.37 | Calculated Property |
| Pvap | 649.53 | kPa | 538.76 | Calculated Property |
| Pvap | 1325.74 | kPa | 587.16 | Calculated Property |
| Pvap | 2409.12 | kPa | 635.55 | Calculated Property |
| Pvap | 4015.15 | kPa | 683.95 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,3-dichloro-.
Mixtures
- 2-Butanone + Benzene, 1,3-dichloro-
- 1-Propanol + 2-Butanone + Benzene, 1,3-dichloro-
- 2-Butanone + 1-Butanol + Benzene, 1,3-dichloro-
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Pentanol
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Hexanol
- N,N-Dimethylacetamide + Benzene, 1,3-dichloro-
- Benzene, 1,3-dichloro- + Dimethyl Sulfoxide
- Benzene + Benzene, 1,3-dichloro- + Hexane, 1-chloro-
- Benzene, 1,3-dichloro- + Pentane, 2,2,4-trimethyl-
- Cyclooctane + Benzene, 1,3-dichloro-
- Octane + Benzene, 1,3-dichloro-
- n-Hexane + Furfural + Benzene, 1,3-dichloro-
- Furfural + Hexadecane + Benzene, 1,3-dichloro-
- Benzene, 1,3-dichloro- + Tetrahydrofuran
- Benzene + n-Hexane + Benzene, 1,3-dichloro-
- Benzene, 1,3-dichloro- + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
- Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
- Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
- Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
- Volumetric, ultrasonic and viscometric studies of binary mixtures of dimethyl sulphoxide with chloro and nitro substituted aromatic hydrocarbons at T = 303.15 K
- Experimental and predicted data of excess molar enthalpies and excess molar volumes for the ternary system (1,3-dichlorobenzene + benzene + 1-chlorohexane) at T = 298.15 K
- The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Measurement and Prediction of Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,3-dichlorobenzene + Benzene + Hexane at 298.15 K.
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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